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Manufacturing method of glucose

A manufacturing method, glucose technology, applied in the field of biochemistry, can solve the problems of poor removal of impurities, reduced service life of resin, low product quality and yield, and achieve the effect of improving utilization rate, prolonging service life and good quality

Active Publication Date: 2012-07-18
SANDA FILM SCI & TECH XIAMEN +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] This production process has the following disadvantages: 1. During the plate-frame or drum filtration process, diatomite and filter residue are continuously discharged and cannot be recycled, and impurities such as protein and fat in the sugar solution cannot be removed well, and the impurities will be Entering the follow-up ion exchange process will bring pollution to the resin and reduce the service life of the resin; second, the regeneration of the resin needs to consume a large amount of acid-base and water, and will produce a large amount of acid-base wastewater, which is seriously polluted; third, the main end product of glucose is fruit Glucose syrup, crystalline glucose and pharmaceutical grade glucose, in order to meet the high purity requirements of pharmaceutical grade glucose, the traditional process can only use recrystallization to improve the purity, so a large number of crystallizers and centrifuges are required, which requires a large investment and land occupation, and requires A large number of operators, low work efficiency and low process yield; 4. On the whole, the traditional production process is a batch operation with a low degree of automation, requiring a lot of manpower, and the product quality and yield are relatively low

Method used

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  • Manufacturing method of glucose
  • Manufacturing method of glucose
  • Manufacturing method of glucose

Examples

Experimental program
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Effect test

Embodiment 1

[0036] Embodiment 1 obtains saccharification liquid (prior art)

[0037]Starch liquefaction: Mix starch and water to prepare a liquid starch emulsion for glucose production. The content of starch accounts for 20%-35% of the total mass of the liquid starch emulsion, and then sterilize to prepare a starch emulsion, and then to the starch emulsion Add high-temperature amylase to the water, spray it once with high pressure from the liquefaction injector, add enzyme twice for continuous liquefaction reaction, and hydrolyze it into a liquefied starch solution with a glucose value between 14% and 25%;

[0038] Saccharification: Cool the liquefied starch solution with a glucose value between 14% and 25% prepared in the previous steps to 35-45°C, then add compound glucoamylase and enzymatically hydrolyze it into a glucose saccharification solution at this temperature. The saccharification solution is stored at a height of about 7.5m and a volume of 120m 3 In the saccharification tank,...

Embodiment 2

[0040] One of embodiment 2 membrane filtration impurity removal

[0041] In this embodiment, Asahi Kasei hollow membrane UMP-153 is used as the microfiltration membrane. The inner diameter of the UMP-153 membrane filament is 2.6mm and the pore diameter is 0.2um. It can be seen from Table 1 that under the operating condition of the inlet pressure of 2.4bar, the concentration is 5-7 times, the membrane basically has no interception of the product, and the flux is maintained between 130LMH-210LMH, and combined image 3 It can be seen that the membrane operation is very stable.

[0042] Table 1 UMP-153 membrane operating data

[0043] the batch

Embodiment 3

[0044] Embodiment 3 Membrane filtration impurity removal

[0045] In this embodiment, Asahi Kasei hollow membrane USP-143 is used as the microfiltration membrane. The inner diameter of the USP-143 membrane filament is 1.4mm and the pore diameter is 0.1um. From the membrane operation data in Table 2, it can be seen that under the operating conditions of an average inlet pressure of about 1.4bar, an average outlet pressure of about 1.1bar, and a circulation flow rate of 1600-2000m3 / h and a temperature of 42-62°C, the concentration to About 6 times, there is basically no interception in the glucose production process, and the membrane flux is between 150-160LMH; combined with the membrane flux change curve, the membrane flux fluctuates between 160LMH, and the repeatability of the three batches is good , indicating that the membrane is very stable in operation; in addition, it can be seen from the test data of the filtrate in Table 5 that in the case of a high liquid-solid content...

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Abstract

The invention discloses a manufacturing method of glucose, comprising the following steps of: (1) liquefying starch: by taking starch as the raw material, liquefying under the action of a liquefying enzyme after size mixing, and then, a glucose saccharified liquid under the action of a saccharifying enzyme; (2) filtering and decontaminating the saccharified liquid by a membrane filtering unit to obtain filtrate, wherein a filtering membrane has the aperture of 1-200nm or the molecular weight cut-off of 10-500kd; (3) carrying out continuous ion exchange on the filtrate by using a moving bed, removing salts to obtain a purified liquid; and (4) filtering the purified liquid by using a nanofiltering membrane to obtain pharmaceutical-grade glucose, wherein a concentrated solution is used for producing daily chemical alcohol or polysaccharose products. Continuous production is adopted in the manufacturing method, and therefore, the production efficiency is high.

Description

technical field [0001] The invention relates to the field of biochemistry, in particular to a method for producing glucose. Background technique [0002] Glucose is an important monosaccharide and an important basic chemical medicine, as well as a raw material for many compounds. The production of glucose has experienced the development process of acid method, acid enzyme method and double enzyme method. see figure 1 , the existing production process for producing glucose is as follows: use starch as raw material, liquefy under the action of liquefying enzyme after pulping, then saccharify through the action of glucoamylase, finally form glucose syrup with DX95%, and then use diatom Soil filtration method enters plate frame or drum for filtration to remove residual starch and suspended matter, then adopts fixed bed ion exchange process, mainly uses a large amount of anion and cation exchange resin to remove the salt in the sugar solution, and finally uses heavy The crysta...

Claims

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Application Information

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IPC IPC(8): C12P19/14B01D61/14B01J47/02B01J47/028
Inventor 林雄水林丽华杜明华李硕林陈建木方富林蓝伟光李斌付吉明
Owner SANDA FILM SCI & TECH XIAMEN
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